Organic liquid fertilizer and process of making

ABSTRACT

A fertilizer derived from an organic source and a method of making are provided. The fertilizer of the present invention advantageously has a Nitrogen content greater than 4%. The method of making the fertilizer also produces potable water.

RELATED APPLICATIONS

This application relates to and claims priority to U.S. ProvisionalPatent Application No. 61/572,751, which was filed on Jul. 21, 2011, andU.S. Provisional Patent Application No. 61/572,749, which was filed onJul. 21, 2011, the contents and teachings of which are incorporatedherein by reference.

BACKGROUND

Adequate nitrogen in the contents of soil is necessary for a healthylawn, plants, and crops. Fertilizers containing nitrogen are used toenhance the nitrogen levels in the soil to produce greener, lusher,faster-growing plants, lawns, and crops. Nitrogen must be available forthe plant to use it, meaning that the nitrogen must be converted to NH₄⁺ or NH₃. The Nitrogen may be readily available or organisms in the soilmust covert the Nitrogen into a usable form.

Inorganic fertilizers, while inexpensive and easy to apply, tend to washthe nutrients out of the soil, requiring reapplication on a regularbasis. Additionally, since inorganic fertilizers are concentrated, theytend to burn plant roots more than organic materials.

Fertilizers that are derived from an organic source are preferable for avariety of reasons. They have a lower burning potential and a lowerleach potential; and they replenish the soil with micro-nutrients,essential amino acids, and organic matter that were consumed by previousagricultural and horticultural activity. However, most fertilizersderived from an organic source have a nitrogen content that is less than3% and the Nitrogen is usually in a slow release form. The slow releasenitrogen in most fertilizer derived from an organic source must bebroken down over time by microorganisms in the soil in order for thatnitrogen to be converted to a form that is usable by plants and crops.This element of organic-derived fertilizer pushes many to purchasesynthetic fertilizers that provide a higher level of nitrogen and aquicker release into the soil and uptake by the plant.

SUMMARY OF THE INVENTION

The present invention provides for a method of making a liquidfertilizer. The method for making fertilizer of the present inventiongenerally includes a) obtaining a liquid organic waste filtrate; b)adding an acid and c) performing an evaporation process on the liquidorganic waste filtrate. The liquid organic waste filtrate originatesfrom a liquid organic waste material wherein the suspended solids havebeen removed. The method of making the liquid fertilizer where themethod starts from liquid organic waste would generally include: a)obtaining liquid organic waste; b) removing the suspended solids fromthe liquid organic waste; c) adding an acid; and d) performing anevaporation process on the liquid organic waste. The liquid organicwaste filtrate is created by obtaining liquid organic waste and removingthe suspended solids. Optionally the method includes a second additionof an acid to adjust the final pH of the liquid fertilizer. The liquidorganic waste is preferably derived from an organic source. This liquidorganic waste is preferably derived from animal manure, specifically,poultry manure.

The present invention also provides for a fertilizer derived from anorganic source with a higher level of nitrogen than other fertilizersderived from an organic source. The fertilizer of the present inventionadvantageously contains at least 4% Nitrogen, which is greater thanprevious organic fertilizer compositions. The Nitrogen in the fertilizerof the present invention is preferably Ammoniacal Nitrogen. ThisAmmoniacal Nitrogen is 100% water soluble and is therefore quicklyreleased into the soil and readily available for plants. Further, thefertilizer of the present invention is derived from an organic source.The fertilizer of the present invention preferably comprises afertilizer that contains from about 4% to 10% nitrogen, more preferablyfrom about 4% to 6% nitrogen. This is a higher nitrogen content thanwhat is presently available in fertilizers that are derived from organicmaterials.

BRIEF DESCRIPTION OF FIGURES

FIG. 1 is a schematic drawing of one embodiment of the method of thepresent invention;

FIG. 2 is a schematic drawing of an additional embodiment of the methodof the present invention; and

FIG. 3 is a schematic drawing of an embodiment that demonstrates themethod of obtaining the liquid organic waste filtrate and the furtherprocessing to the ultimate end product.

DETAILED DESCRIPTION

A method of making a liquid organic fertilizer is provided. The methodgenerally comprises the following steps: a) obtaining a liquid organicwaste filtrate; b) adding an acid to the liquid organic waste filtrate;and c) performing an evaporation process on the liquid organic wastefiltrate.

A further embodiment provides a method for making fertilizer thatincludes the steps of: a) obtaining liquid organic waste; b) removingsuspended solids from the liquid organic waste, forming a liquid organicwaste filtrate; c) adding an acid; and d) performing an evaporationprocess on the liquid organic waste filtrate. In an alternateembodiment, the method further comprises the step of adding a secondacid. Preferably, this second acid is added after the evaporationprocess is performed on the liquid organic waste filtrate.

The liquid organic waste can be any aqueous solution that contains adissolved protein, Ammoniacal Nitrogen, and other soluble nutrients. Ifthe organic waste is in a solid or semi-solid form, water is preferablyadded to the solid or semi-solid material to form a fluid mixture. Forexample, in an embodiment where animal manure is utilized, water isadded to form a fluid mixture creating liquid organic waste. The waterpreferably creates a fluid mixture of water and suspended and dissolvedsolids making up the liquid organic waste. An effluent discharge from ananaerobic digester is a preferred liquid organic waste. The suspendedand dissolved solids in the liquid organic waste preferably include, butare not limited to: nitrogen, phosphate, potash, secondary nutrients,micro-nutrients and organic matter found in anerobically digested manureor other agriculturally related organic waste. The temperature ofstarting material is preferably between 90° F. and 140° F., morepreferably from about 132° F. to 136° F. This temperature is preferablyachieved using a heat exchanger. The liquid organic waste for the methodof the present invention is preferably derived from an organic source.The liquid organic waste is preferably derived from natural sources theinclude, but are not limited to, plant and animal-biproducts, rockpowders, seaweed, inoculants, conditioners, dairy product waste,livestock manure, liquid manure, worm castings, peat, guano, compost,blood meal, bone meal, fish meal, decomposing crop residue, cheese whey,dairy product waste, livestock manure, mixed liquor from food andlivestock processing facilities, wastewaters from a variety of foodprocessing operations, and combinations thereof. However, the listprovided herein is not meant to be limiting, as any natural source thatprovides nitrogen, phosphate, and potash will work for purposes of thepresent invention.

The liquid organic waste is preferably filtered to remove suspendedsolids. The removal of suspended solids from the liquid organic wastecreates the liquid organic waste filtrate. This liquid organic wastefiltrate preferably contains less than 2,000 parts per million(hereinafter “ppm”) suspended solids, more preferably, less than 1,500ppm suspended solids, and most preferably 1,200 ppm suspended solids orless. The liquid organic waste filtrate preferably contains nitrogen,phosphate, potash, secondary nutrients, micro-nutrients and organicmatter. The nitrogen is preferably Ammoniacal Nitrogen.

The step of removing suspended solids can be performed by any mechanismcapable of filtering particles. The suspended solids are preferablythose particles that won't pass through a 270 Dalton membrane under 500psi of pressure. The removal of suspended solids can preferably becompleted using at least one, at least two, or at least three or morefiltration steps. The removed suspended solids can be further processedto produce granular fertilizers. These filtration steps may utilize thesame method of filtration or different methods of filtration.Preferably, in an embodiment where three filtration steps are performed,the first step removes large suspended solids (greater than 24 microns),the second step removes small suspended solids (less than 24 microns),and the third step removes any residual solids. Preferably, thesuspended solids are removed using one or more filtration mechanismsincluding, but not limited to, mechanical screening, microfiltration,ultrafiltration, nanofiltration, reverse osmosis, membrane separation,and electro-coagulation. Preferred machinery for removing suspendedsolids include, but are not limited to, BioPulse system provided bybioprocess H2O (Portsmith, R.I.); Petro Membrane Bioreactor (“MBR”)(Siemens Industry, Inc. USA); PURON MBR (Koch Membrane Systems, Inc.,Wilmington, Mass.); Pall Aria Integrated MF/NF(microfiltration/nanofiltration) and MF/RO (microfiltration/reverseosmosis) systems (Pall Corporation, Port Washington, N.Y.); Alfa LavalFiltration (Alfa Laval, Sweden); and NF (nanofiltration) and RO (reverseosmosis) Membrane Separation (BKT Co Ltd, Korea). The filtration step(s)result in the liquid organic waste filtrate.

In a further embodiment, the step of removing suspended solids furtherincludes a second filtration step. This second filtration steppreferably removes any material of a size that may disrupt, impeded, orblock an irrigation system. Any filtering process that removes thematerial of a size that might disrupt an irrigation system would workfor purposes of the present invention. Preferred filtering processesinclude, but are not limited to, the use of a 500-mesh screen, membranefilters, continuous agitation through turbulent flow, or reverseosmosis, with or without a self-cleaning method of filtration.

In yet a further embodiment, the step of removing suspended solidsincludes a third filtration step. The third filtration step can be anyfiltration method referenced herein, however, it is preferred that it isreverse osmosis.

An acid is preferably added to the liquid organic waste filtrate.Preferably, the acid is utilized to adjust the pH of the liquid organicwaste filtrate to a pH of 7 or lower. Preferably, the pH is adjusted toa pH of between pH 3 to pH 7, more preferably from about pH 5 to pH 7,and most preferably about pH 6.5. Additionally, the acid preferably actsto bind the ammonium molecules so that they are able to release freeammonia, preferably without producing suspended solids. In an embodimentwhere an acid is utilized, the acid can be any organic or inorganic acidthat will adjust the pH of the liquid organic waste filtrate to a pH 7or less, more preferably a pH of 6.5. The type and amount of acid willvary depending on the given situation, but the amount and type of acidis enough to lower the pH of the liquid organic waste filtrate to a pHof 7 or less. The acid is preferably selected from, but is not limitedto, citric acid, lactic acid, L-malic acid, vinegar (acetic acid),phosphoric acid, sulfuric acid, hydrochloric acid, nitric acid, andcombinations thereof. Most preferably, the acid is citric acid. In amost preferred embodiment, the acid utilized is an organic acid. Anyorganic acid will work for purposes of the present invention. Preferredorganic acids include, but are not limited to, lactic acid, acetic acid,formic acid, citric acid, oxalic acid, and uric acid. Inorganic acidsmay also be utilized for purposes of the present invention. Inorganicacids include, but are not limited to, hydrochloric acid, nitric acid,phosphoric acid, sulfuric acid, hydrofluoric acid, hydrobromic acid,perchloric acid, and combinations thereof. The acid is preferably addedin an amount that is sufficient to change the pH of the liquid organicwaste filtrate to a pH 7 or lower. The amount of acid added depends onthe type of acid used, starting pH of the liquid organic waste filtrate,the buffering capacity of the liquid organic waste filtrate, and theNitrogen content of the liquid organic waste filtrate. In a preferredembodiment the acid is added in an amount of from about 0.1 lb/gallon to2.0 lb/gallon, more preferably from about 0.2 lb/gallon to 1.5lb/gallon, still more preferably from about 0.4 lb/gallon to 1.0lb/gallon, and most preferably, the acid is added in an amount of about0.6 lb/gallon.

The liquid organic waste filtrate and acid are preferably exposed to anevaporation process. The evaporation process may be any process suitablefor removing water from the composition. In a preferred embodiment, thecomposition is in a liquid form following the evaporation step.Preferably, a vacuum evaporation is utilized. A most preferred vacuumevaporator is the Turbo CAST® vacuum evaporator (ThermoEnergy Inc.,Worcester, Mass.). Other possible vacuum evaporators include, but arenot limited to, the vacuum evaporators made by Veolia Water Solutionsand Technologies (Cary, N.C.), HF Pure Water (Compton, Calif.),Mech-Chem Associates (Norfolk, Mass.), and Econ Industries (Starnberg,Germany). The evaporation process requires heat to remove water from thecomposition. The temperature range of the evaporation process ispreferably from about 90-110° F., more preferably from about 100-105° F.In an embodiment that includes a vacuum evaporation process, the vacuumrange is preferably from about 26-28 inches of mercury, with thepreferred range being from about 27-28 inches of mercury. The time theevaporator is used depends on the temperature and pressure utilized andcan be determined in line with industry standards. A non-limitingexample includes a Turbo Cast MVR 21000 system (ThermoEnergy, Inc.,Worcester, Mass.), operating at 100° F. and 28 inches of mercury, willconcentrate 155,000 gallons of solution to 21,000 gallons by removingwater at a rate of 46,565 pounds per hour.

Preferably, the evaporation process creates water vapor that can becaptured and transformed into potable water. Advantageously, during theevaporation step, water vapor is created. This water vapor is thencooler condensed into liquid water. The water that results from themethod of the present invention is clean and suitable for drinking.

An alternate embodiment of the present invention is described in thenext several paragraphs. The alternate embodiment starts with ananerobic digester discharge (herinafter “digestate”). This digestate canbe any fluid mixture of water and suspended and/or dissolved solids. Thesuspended and dissolved solids in the digestate preferably include, butare not limited to nitrogen, phosphate, potash, secondary nutrients,micro-nutrients and organic matter found in anerobically digested manureor other agriculturally related organic waste. Preferably, the digestateis at a temperature of between 80° F. and 132° Fahrenheit.

The digestate is preferably then processed by a filtering mechanism toremove and capture the large suspended solids, hereinafter called“recovered solids”. These large suspended solids are preferably greaterthan 24 microns in size. The recovered solids preferably have a moisturecontent of from about 70% to 90% moisture, more preferably about 80%moisture. The recovered solids are then preferably processed in atwin-screw helical heat exchanger to produce granular fertilizer with amoisture content of 10% or less, more preferably 5% or less. The heatutilized to process the recovered solids is preferably from an indirectsource, such as, but not limited to hot oil flowing around the ducts.Preferably, the rotation of helical ducts severs to cause the solids tobind together to form fertilizer granules. Amonia-rich exhaust gas ispreferably created by this process that can be cooled and added to theliquid filtrate and further processed. The formation of granularfertilizer is an optional part of the method of the present inventionand is not a required element. In an alternate embodiment, the recoveredsolids are discarded.

In one embodiment, the liquid filtrate remaining after the suspendedsolids are removed is pH adjusted with an acid to produce a pH ofapproximately 7.0. The acid added can be any acid capable of adjustingthe pH of the liquid filtrate. Preferably an organic acid is used, morepreferably citric acid is utilized. The liquid filtrate is preferablythen filtered at least one additional time, more preferably at least twoadditional times. The first additional filtration step preferablyremoves the remaining small suspended solids. The small suspended solidsare preferably less than or equal to 24 microns. This first additionalfiltration step is preferably completed using membrane filters, however,any filtration system capable of removing small suspended solids willwork. Other filtration methods contemplated by the present invention arediscussed herein. The second additional filtration step preferablyremoves molecular dissolved solids. This second additional filtrationstep is preferably completed using a nano-filter, however, anyfiltration system capable of removing molecular dissolved solids, suchas those filtration methods discussed herein.

The liquid organic waste filtrate resulting from the above process is aliquid fertilizer product with unique solids and nutrient content ofexceptional value for soil conditioning, replacement of exhaustednutrients, and restoration of soil health. The second filtration step isa semi-continuous process that produces reject in quantifiable batchvolumes. After a programmed interval, the valve of the extruder isopened to release the accumulated reject. This accumulated reject isisolated and removed to storage. At this point, the next batch of liquidorganic waste is filtered. This cycle repeats indefinitely. Citric acidis preferably added to the resulting liquid filtrate from the secondfiltration step to adjust the pH. This pH adjustment preferablystabilizes the ammonium nitrogen contained in the permeate and producesentrained carbon dioxide. The carbon dioxide gas is liberated from theliquid filtrate and then the acidified liquid filtrate is filtered againin the third additional filtration step. The concentrated streamproduced by the third filtration step is then concentrated by vacuumevaporation. This vacuum evaporation further concentrates the liquidorganic waste filtrate from the second filtration step and produces thephosphate-free liquid organic fertilizer of the present invention. Thewater vapor produced during this process is preferably condensed andcombined with permeate obtained from the final filtration step. Theresultant solution is clean water of such quality required to meet theNPDES discharge permit requirements established by the USEPA Clean WaterAct of 1972.

The final products of this alternate embodiment of the method of thepresent invention are preferably a liquid fertilizer and water. Theliquid fertilizer preferably has a high Nitrogen content, where theNitrogen is Ammoniacal Nitrogen, which is 100% water soluble and readilyavailable to the soil. Additionally, the water produced is potablewater.

A liquid fertilizer derived from an organic source is also provided bythe present invention. The organic source preferably includes, but isnot limited to, plant and animal-bi-products, rock powders, seaweed,inoculants, conditioners, dairy product waste, livestock manure, liquidmanure, worm castings, peat, guano, compost, blood meal, bone meal, fishmeal, decomposing crop residue, cheese whey, dairy product waste,livestock manure, mixed liquor from food and livestock processingfacilities, wastewaters from a variety of food processing operations,and combinations thereof. However, the list provided herein is not meantto be limiting, as any natural source that provides nitrogen, phosphate,and potash will work for purposes of the present invention. In a mostpreferred embodiment, the organic source is animal manure, mostpreferably, poultry manure.

The liquid fertilizer of the present invention preferably containsAmmoniacal Nitrogen derived from an organic source. The AmmoniacalNitrogen provided by the fertilizer of the present invention is derivedfrom anerobically digested waste. The Ammoniacal Nitrogen in the liquidfertilizer of the present invention is preferably soluble AmmoniacalNitrogen (N—NH4) that is immediately available to the plant. TheAmmoniacal Nitrogen is preferably present in the liquid organic wasteand thus, still present in the liquid organic waste filtrate. TheAmmoniacal Nitrogen is preferably concentrated by the method of thepresent invention and the addition of the acid in the method also bindsthe ammonium (NH₄) molecules very tightly, thus restricting theirconversion to free ammonia (NH₃) and subsequent loss throughvolatilization.

This Ammoniacal Nitrogen is preferably present in the liquid fertilizerin an amount of greater than 4%, more preferably from about 4% to 10%Nitrogen, more preferably from about 4% to 6% Nitrogen, and mostpreferably about 6% Nitrogen. Water is preferably present in the liquidfertilizer in an amount of from about 10% to 90%, more preferably fromabout 20% to 80%, more preferably from about 30% to about 60%, and mostpreferably from about 35% to 45%. Advantageously, the liquid fertilizercontains dissolved solids. Preferably, the liquid fertilizer contains atleast 40,000 ppm to about 750,000 ppm dissolved solids, more preferablyfrom about 100,000 ppm to about 700,000 ppm dissolved solids, preferablyfrom about 200,000 ppm to 690,000 ppm dissolved solids, more preferablyfrom about 300,000 ppm to about 680,000 ppm dissolved solids, and mostpreferably from about 550,000 ppm-650,000 ppm dissolved solids. It isgenerally preferred that the liquid fertilizer contain at least 40,000ppm of dissolved solids. A preferred embodiment contains about 590,000ppm dissolved solids.

In a preferred embodiment, the liquid fertilizer has little to nosuspended solids in the composition. Preferably, the liquid fertilizerhas from 0 ppm to 20,000 ppm suspended solids, more preferably less than15,000 ppm, more preferably less than 13,000 ppm and most preferablyless than 12,000 ppm, more preferably less than 10,000 ppm, still morepreferably less than 5,000 ppm, still more preferably less than 3,000ppm, and most preferably about 1,200 ppm. In a most preferred embodimentthe liquid fertilizer has no suspended solids. The liquid fertilizer ofthe present invention may also contain potash. The potash is preferablysoluble potash. The potash is preferably present in an amount from about1% to 10%, most preferably about 5%. Sulfur may also be present in theliquid fertilizer. Sulfur is preferably present in the liquid fertilizerin an amount less than 10%, more preferably less than 8%, and mostpreferably 4% or less.

The fertilizer of the present invention preferably has a pH of betweenpH 3 to pH 7, more preferably from about pH 5 to pH 7, and mostpreferably about pH 6.5. Additionally, the fertilizer of the presentinvention is preferably free of pathogens. In a preferred embodiment,pathogens die within 24 hours of being introduced into the fertilizer.

Additionally, the fertilizer of the present invention may be certifiedby the United States Department of Agriculture (“USDA”) as “USDAorganic.” The USDA has a program called the National Organic Program(“NOP”) which specifically describes the synthetic materials that areallowed in fertilizer (www.ams.usda.gov/nop). Specifically, the list ofacceptable ingredients is provided in the National Organics Program Listin section 205.605. In a preferred embodiment, the method of the presentinvention produces a liquid fertilizer eligible for USDA organiccertification. However, this is not a required element of the presentinvention. The method of the present invention producing a fertilizer ofthe present invention can be derived from an organic source withoutmeeting the requirements of being certified USDA organic.

Definitions

“Organic” or “Organically derived”, for purposes of the presentinvention refer to the natural source of the starting material for thefertilizer of the present invention. While not meant to be limiting, astarting material for the fertilizer may include, but is not limited toplant and animal bi-products, rock powders, seaweed, inoculants,conditioners, dairy product waste, livestock manure, liquid manure, wormcastings, peat, guano, compost, blood meal, bone meal, fish meal,decomposing crop residue, cheese whey, dairy product waste, livestockmanure, mixed liquor from food and livestock processing facilities,wastewaters from a variety of food processing operations, andcombinations thereof. However, the list provided herein is not meant tobe limiting, as any natural source that provides nitrogen, phosphate,and potash will work for purposes of the present invention.

“USDA organic” refers to a fertilizer or components that meet theguidelines as set forth by the USDA requirements to certify something as“organic.”

“Ammoniacal Nitrogen” for purposes of the present invention refers toNitrogen that is provided to the plant in a water soluble form, wherethe Ammoniacal Nitrogen includes ammonium (NH₄ ⁺) and ammonia (NH₃). TheAmmoniacal Nitrogen is readily plant available.

“Liquid organic waste,” for purposes of the present invention refers toany aqueous solution that contains a dissolved protein, AmmoniacalNitrogen, and other soluble nutrients. If the waste is in a solid orsemi-solid form, water is preferably added to the solid or semi-solidmaterial to form liquid organic waste, creating a fluid mixture of waterand suspended and dissolved solids. The liquid organic waste can comefrom any organically derived source, as detailed in the definition for“organic” or “organically derived.”

“Liquid organic waste filtrate,” for purposes of the present invention,is the liquid organic waste, described above, where the suspended solidshave been removed. Preferably, the suspended solids are removed by afiltration process.

“Suspended solids,” for purposes of the present invention refer to thoseparticles that won't pass through a 270 Dalton membrane under 500 psi ofpressure.

“Dissolved solids,” for purposes of the present invention refer to thoseparticles that are smaller than the suspended solids, or those particlesthat will pass through a 270 Dalton membrane under 500 psi of pressure.

EXAMPLES Example 1

This example illustrates one embodiment of the method and fertilizer ofthe present invention.

Materials and Methods

Poultry manure was obtained and water was added to the poultry manure toform an aqueous mixture for the liquid starting material. Ananofiltration and reverse osmosis filtration system were used to removethe suspended solids. Once the suspended solids were removed, citricacid was added to the liquid starting material. Next, a vacuumevaporator was utilized at between 100-105° F. at a pressure of 26-28inches of mercury. After the evaporation process was complete, anadditional amount of citric acid was added to adjust the pH of thesolution to around pH 6.5. The water vapor from the evaporation processwas captured.

Results and Conclusions

The resulting liquid fertilizer contained a soluble and rapid-actingnitrogen source, where the amount of nitrogen in the fertilizer was 6%.The potassium content of the fertilizer was 5% and the fertilizer didnot contain any phosphorus. The potash content was about 5% and thefertilizer contained 4% sulfur. Suspended solids were present in thefertilizer at about 1,200 ppm and the fertilizer contained about 590,000suspended solids. The organic matter present in the fertilizer was about75% and it was about 11 pounds per gallon at 68° F. The liquidfertilizer was also pathogen free.

Additionally, the water vapor was recovered as potable water, suitablefor drinking.

Example 2

This example illustrates use of the fertilizer for crops.

Materials and Methods

Using the fertilizer resulting from Example 1, crops may be fertilized.The crops may be fertilized at 10 lbs N/acre pre-plant or at planting;25-35 lbs N/acre at thinning; and 10-15 lbs N/acre at pre-harvest.

Results and Conclusions

The total nitrogen in the fertilizer will be 45-60 lbs N/acre, where thefertilizer of the present invention has 0.66 lbs N/gallon, which equals75-100 gallons/acre.

Example 3

This example illustrates the pathogen-free aspect of the fertilizer ofthe present invention.

Materials and Methods

Pathogens may be introduced into the liquid fertilizer of the presentinvention.

Results and Conclusions

After 24 hours, none of the pathogens introduced into the liquidfertilizer will be alive.

Example 4

This example illustrates the removal of suspended solids.

Materials and Methods

The solid separation and nutrient recovery process began with theeffluent discharge from an anaerobic digester, hereafter referenced as“digestate”. Digestate is a fluid mixture of water and suspended anddissolved solids including, but not limited to: nitrogen, phosphate,potash, secondary nutrients, micro-nutrients and organic matter found inanaerobically digested manure or other agriculturally related organicwaste. The temperature of digestate was between 80° F. and 132°Fahrenheit.

The digestate was processed by a filtration mechanism to remove andcapture large (>24 microns) suspended solids, hereafter referenced as“recovered solids”. The recovered solids were separated from thedigestate by the filtration mechanism have a moisture content ofapproximately 80 percent. These wet solids were then processed in atwin-screw helical heat exchanger to produce granular fertilizer with amoisture content of 5% or less. The wet recovered solids were thenintroduced into a series of rotating helical ducts. Hot oil flowingaround through the ducts provided indirect heat. The constant motion andheat applied to the solids functioned to remove latent moisture from thesolids. Rotation of the helical ducts served to cause the solids to bindto each other and form granules of solid fertilizer. These fertilizergranules may be later screened to size as desired. The evaporatedmoisture consisted of an ammonia-rich exhaust gas. This warm gas may becooled to produce condensate that can be added to the filtrate from thefiltering mechanism and further processed.

Example 5

This example illustrates the filtration process of the presentinvention.

Materials and Methods

The filtrate from the filtration mechanism was pH adjusted with citricacid to produce a pH of approximately 7.0 and then fed through a seriesof membrane filters hereafter referenced as “filtration steps”. Thefirst filtration step (nano-filtration) removed the remaining small (<24microns) suspended solids that were not initially captured. The secondfiltration step (reverse osmosis) removed molecular dissolved solidsthat pass through the nano-filter.

The material that passed through each filtration step, hereafterreferenced as “permeate”, was the feed stream to the subsequentfiltration step. The concentrated product produced at each filtrationstep, hereafter referenced as “reject”, was a high-value fertilizerproduct of unique solids and nutrient content. After a programmed timeinterval, a valve was opened to release the accumulated reject. Thevalve was then closed to allow the concentration of additional feedstream. This cycle repeated several times. The filtration methodutilized continuous agitation through turbulent flow forced the filtrateagainst the membrane filters of a cylindrical mechanism. As themechanism rotated, specially designed blades created vortices whichremoved foulants from the membrane surface and dramatically decreasedboundary layer effects. Both reject and permeate were obtained andprocessed as previously disclosed.

Citric acid was added to the reject from the second filtration step(reverse osmosis) to produce approximately 6.0 pH. This pH adjustmentstabilized the ammonium nitrogen contained in the reject and, in doingso, produced entrained gaseous carbon dioxide. Entrained gas wasliberated from the reject by applying ultrasonic vibration andmechanical agitation. The acidified, de-gassed reject was furtherconcentrated by vacuum evaporation.

The vacuum evaporation process was operated under vacuum ofapproximately 28 inches mercury and at a temperature of approximately100° Fahrenheit. This process further concentrated the reject solutionand produced a phosphate-free liquid organic fertilizer. Nitrogen andpotash concentrations may be adjusted as required by controlling thevolume of water removed through evaporation. The water vapor produced byevaporation was condensed and combined with permeate obtained from thefinal filtration step. The resultant solution was then processed byspiral reverse osmosis which removes any remaining solids and anypathogens not destroyed in the digestion process.

Results and Conclusions

The final products of the filtrate processing consisted of: at least twohigh-value liquid fertilizer products with uniquely different nutrientcontents and agronomic uses, including a concentrated phosphate-freeliquid organic fertilizer, and potable water.

Example 6

This example provides another embodiment of the present invention.

Materials and Methods

A typical pilot process demonstration included the collection of 300gallons of digestate from the anaerobic digestion of poultry waste at132° Fahrenheit. This stream had a total nitrogen content of 14 percent(dry weight basis) including an ammonium concentration of approximately3,000 ppm. This stream was mechanically screened to remove large (>24microns) suspended solids. The underflow from the mechanical screen wasapproximately 294 gallons with an ammonium concentration ofapproximately 2,800 ppm.

The 294 gallons was then filtered to remove the residual suspendedsolids greater in size than will pass through a 270 Dalton membraneunder 500 psi pressure. This filtration step produced approximately 44gallons of reject and 250 gallons of permeate. The ammoniumconcentration of the permeate stream was approximately 2,000 ppm.

The 250 gallons of permeate were pH adjusted with citric acid to 6.5 andthen filtered by reverse osmosis. The reverse osmosis process producedapproximately 37 gallons of reject and 213 gallons of permeate (liquidorganic waste filtrate). Approximately 0.6 pounds of citric acid wereadded per gallon of reject produced. The ammonium concentration of thereject stream was approximately 15,000 ppm.

The 37 gallons of reject from the reverse osmosis process were thenconcentrated to approximately 6 gallons of finished product by the useof vacuum evaporation.

Results and Conclusions

The fertilizer of the present invention was produced. The ammoniumconcentration of the finished product was 60,000 ppm or six percent byweight.

All of the compositions and methods disclosed and claimed herein can bemade and executed without undue experimentation in light of the presentdisclosure. While the compositions and methods of this invention havebeen described in terms of preferred embodiments, it will be apparent tothose of skill in the art that variations may be applied to thecompositions and methods and in the steps or in the sequence of steps ofthe method described herein without departing from the concept, spiritand scope of the invention. More specifically, it will be apparent thatcertain agents which are both chemically and physiologically related maybe substituted for the agents described herein while the same or similarresults would be achieved. All such similar substitutes andmodifications apparent to those skilled in the art are deemed to bewithin the spirit, scope and concept of the invention as defined by thefollowing claims.

1. A method for making a liquid fertilizer comprising the steps of: a)obtaining an liquid organic waste filtrate; b) adding an acid; and c)performing an evaporation process on the liquid organic waste filtrate.2. The method of claim 1, wherein the method further comprises the stepof adding a second acid after performing the evaporation process tocreate a liquid fertilizer.
 3. The method of claim 1, wherein the acidis citric acid.
 4. The method of claim 3, wherein the citric acid isadded in an amount of from about 0.1 lbs/gallon to 2.0 lbs/gallon. 5.The method of claim 1, wherein the liquid organic waste filtratecontains Ammoniacal Nitrogen.
 6. The method of claim 1, wherein the acidis added in an amount sufficient to change the pH of the liquid organicwaste filtrate to a pH 7 or less.
 7. The method of claim 1, wherein theliquid organic waste filtrate is produced by the steps comprising: a)obtaining liquid organic waste; and b) removing suspended solids.
 8. Themethod of claim 7, wherein the step of removing the suspended solids isperformed by a filtration mechanism.
 9. The method of claim 7, whereinthe liquid organic waste filtrate contains less than 1,200 ppm suspendedsolids.
 10. The method of claim 7, wherein the removed suspended solidsare particles that will not pass through a 270 Dalton membrane under 500psi of pressure.
 11. The method of claim 7, wherein the liquid organicwaste comprises poultry manure and water.
 12. A method for making aliquid fertilizer comprising the steps of: a) obtaining liquid organicwaste; b) removing suspended solids from the liquid organic waste; c)adding an acid; and d) performing an evaporation process.
 13. The methodof claim 12, wherein steps a) and b) form a liquid organic wastefiltrate.
 14. A liquid fertilizer comprising at least 4% Nitrogen,derived from a liquid organic waste filtrate starting material.
 15. Theliquid fertilizer of claim 14, wherein the Nitrogen content is 6%. 16.The liquid fertilizer of claim 14, wherein said liquid fertilizer isfree of pathogens.
 17. The liquid fertilizer of claim 14, wherein theliquid fertilizer contains about 5% potash.
 18. The liquid fertilizer ofclaim 14, wherein the liquid fertilizer contains about 590,000 ppmdissolved solids.
 19. The liquid fertilizer of claim 14, wherein theorganic starting material is animal manure.
 20. The liquid fertilizer ofclaim 19, wherein the animal manure is poultry manure.
 21. The liquidfertilizer of claim 14, wherein the Nitrogen is in a form available toplants.
 22. The liquid fertilizer of claim 14, wherein the liquidfertilizer meets the criteria for USDA organic certification.